US8364453B2 - Method and apparatus for describing the statistical orientation distribution of particles in a simulation of a mould filling process - Google Patents
Method and apparatus for describing the statistical orientation distribution of particles in a simulation of a mould filling process Download PDFInfo
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/76—Measuring, controlling or regulating
- B29C45/7693—Measuring, controlling or regulating using rheological models of the material in the mould, e.g. finite elements method
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/0005—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor using fibre reinforcements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/06—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
- B29K2105/12—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts of short lengths, e.g. chopped filaments, staple fibres or bristles
- B29K2105/14—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts of short lengths, e.g. chopped filaments, staple fibres or bristles oriented
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/06—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
- B29K2105/16—Fillers
- B29K2105/18—Fillers oriented
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Definitions
- the present invention relates to the field of three-dimensional modelling of a flow of a particle containing suspension into a mould cavity, and more specifically to a method and apparatus for describing the statistical orientation distribution of nonspherical particles in a simulation of a process wherein a mould cavity is filled with a suspension that contains a large number of nonspherical particles.
- a true 3-D simulation of an injection moulding process or a metal casting process involves a system of up to several hundred thousands of equations. Progress has been made in the past to improve the efficiency of the simulation methods to cope with these complex calculations. With optimized software and the processing power of modern workstations such simulations can be performed in a workplace, i.e. the results are obtained fast enough to be suitable outside the purely scientific research area and can be applied by engineers in research and development departments, foundries and manufacturers of injection moulded articles.
- fibre reinforced parts it is often crucial for development engineers to have a description of the fibre orientation distribution to be able to predict tension and warping aspects of the component.
- fibres are used to improve the mechanical properties of plastic parts. But then the (thermo-) mechanical properties (like thermal expansion, strength and stiffness) depend on the orientation of the fibres.
- Injection moulded fibre reinforced parts are replacing structural metallic components because they offer an improved strength/weight ratio, durability, component integration and lower costs.
- Computer aided engineering simulation can be used advantageously to provide design and manufacturing engineers with visual and numerical feedback as to what is likely to happen inside the mould cavity during the injection moulding process, allowing them to better understand and predict the behaviour of contemplated component designs so that the traditional, costly trial and error approach to manufacturing can be eliminated substantially.
- the use of computer aided engineering simulation facilitates optimizing component designs, mould designs, and manufacturing processing parameters during the design phase, where necessary changes can be implemented readily, with the least cost and impact on schedule.
- CAE simulation techniques within the engineering process for fibre reinforced components encompasses (i) a simulation of the “injection moulding” manufacturing process including the computation of fluid flow and heat transfer and (ii) stress & strength (and possibly durability) calculations, all performed on the macroscopic level, for these components to determine their functional mechanical properties under external loads. Both types of simulation require suitable material models describing the properties of the polymer material containing the immersed fibres in liquid as well as in the solid state.
- the length scale on the macroscopic level are determined by the linear dimensions (overall size, wall thicknesses etc.) of the component geometry typically varying in the range of a few mm up to cm.
- the dimensions of the computational cells have to resolve the macroscopic length scales with sufficient accuracy, therefore they are typically up to one order of magnitude smaller than the smallest macroscopic dimension.
- the typical dimensions of the immersed fibres in short-fibre reinforced parts are one or two orders of magnitude below the typical dimensions of the macroscopic computational cells, the fibre properties, which are relevant to the modelling of the macroscopic material behaviour are described by a statistical approach.
- the mathematical model describing the FO distribution in terms of its moments is significantly simplified by means of an approximate computation of the 4 th order orientation tensor in terms of the 2 nd order tensor in terms of a closure relation.
- a closure relation provides the mathematical description of such a computational scheme in terms of a function, and the related computational procedure is denoted as “closure approximation” if a closure relation is only approximately valid under specific assumptions.
- the approach using only the 2 nd order FO tensor together with some closure approximation leads to a model of “Folgar-Tucker” type to simulate the evolution of the 2 nd order FO tensor in time and space during the mould filling process (see sections 2.2 to 2.5 of the detailed description for details).
- the document “Glass fibre orientation within injection moulded automotive pedal—Simulation and experimental studies, B. R. Whiteside et Al, Plastics, Rubber and Composites, 2000, Volume 29, No. 1” discloses a method for modelling the fibre orientation distribution within a reinforced thermoplastic article using on the asymmetric thermoplastic flow and analysis containing a fibre orientation prediction algorithm.
- the software approximated a three-dimensional model using a two-dimensional finite element mesh consisting of linear triangular elements.
- Flow fields were calculated using the generalized Hele-Shaw approximation and a variation of the Folgar-Tucker equation to calculate fibre orientation.
- Fibre orientation, temperature and viscosity calculations were performed using a finite difference technique over 19 laminates through the “thickness” of each element in order to produce a three dimensional solution.
- this system could not be described as truly three-dimensional because the model cannot simulate velocity components in the out of plane direction (a limitation of the Hele-Shaw approximation).
- the method described in this document would, when adapted to true three-dimensional simulation, result in a unstable and too much processing power consuming simulation that could not be used in the workplace of e.g. development engineers.
- This object is achieved in accordance with claim 1 by providing a computer implemented method for calculating orientation statistics of nonspherical particles on a macroscopic level by use of a simulation model for simulating an injection moulding process in which a mold cavity, which forms at least part of the geometry of a simulation domain, is filled or partly filled with a suspension that is formed by a solvent containing a large number of nonspherical particles, wherein a digital representation or computer model of the geometry of the simulation domain is provided, and wherein a mesh with a plurality of computational cells is formed by subdividing or discretizing at least part of the simulation domain, the method comprising the steps of a) specifying boundary conditions; b) setting initial conditions; c) solving the balance equations for mass, momentum and energy for at least a portion of the cells of the simulation domain to obtain fluid flow, heat flow and mass transfer at a macroscopic level; and d) solving nonspherical particle orientation dynamic equations based at least partly on the results of the solved balance equations to thereby determine changes in
- step c) further comprises (cc) determining an updated free surface or flow front of the fluid or suspension, which free surface separates cells filled with the suspension from the empty cells of the cavity, based at least partly on the results of the solved balance equations.
- step (cc) further comprises updating the boundary conditions in accordance with the updated flow front.
- the method of the invention further comprises the steps of e) determining if the simulated injection moulding process is finished by determining if the mold cavity is filled by the simulated injection of the suspension; and f) repeating steps c), cc) and d) until the simulated injection moulding process is finished.
- This object of the present invention is also achieved by providing a method for describing the statistical distribution orientation of nonspherical particles in a simulation of a process wherein a mold cavity is filled with a suspension that is formed by a solvent that contains a large number of nonspherical particles, the method comprising (1) providing a three dimensional computer model defining the geometry of the cavity; (2) specifying the boundary conditions; (3) discretizing a solution domain based on the model to form a mesh with a plurality of cells; (4) solving the energy and flow equations for at least a portion of the solution domain; (5) computing flow and temperature conditions in the respective cells as a function of time; (6) compute the changes in nonspherical particle orientation; and (7) describing the statistical distribution of the orientation of the nonspherical particles in the respective cells as a function of time.
- the methods of the invention utilize the suspension flow to predict the fibre orientation distribution and thermo-mechanical properties throughout the part at a substantially reduced computational effort.
- the data resulting from the simulation may be provided in human readable form to a development engineer, who can thereby optimize the products in relation to the fiber orientation and thus improve the strength and shape stability of the article.
- FIG. 1 a cross sectional view through a diagrammatic representation of an injection moulding machine including a mould
- FIG. 2 is a top level flow chart summarizing basic process steps of an injection moulding process according to an embodiment of the invention
- FIG. 3 is a flowchart illustrating in further detail step 5 of the flowchart of FIG. 2 ;
- FIG. 4 is a micrograph of a fibre reinforced plastic article
- FIG. 5 illustrates a model of a fibre used in an embodiment of the invention
- FIG. 6 is a graph illustrating the quadratic & cubic and the linear & constant terms of the characteristic polynomial
- FIG. 7 is a graph illustrating the triple of eigenvalues of the matrix
- FIG. 8 shows a special example corresponding to a “maximally symmetric” case
- FIG. 9 shows distorted versions of the tetrahedron-shaped volume
- FIG. 10 shows a picture of the overall structure of the phase space set M FT of FO matrices (i.e. 2 nd order FO tensors) according to an embodiment of the invention
- FIG. 11 is a flowchart illustrating the operator splitting process is in a simplified form according to an embodiment of the invention.
- FIG. 12 is a flowchart illustrating the details of the time stepping method.
- FIG. 13 is a flowchart illustrating a phase space projection process using trace rescaling according to an embodiment of the invention.
- FIG. 1 shows diagrammatically an injection moulding machine 1 .
- the injection moulding machine is provided with a screw 2 that is fed with polymer pellets disposed in a hopper 3 .
- the polymer pellets are by the action of the screw 2 and heating elements 4 transformed to a viscous mass that is urged under high pressure into a mould cavity 5 in the mould 6 .
- moulding machine and the injection moulding manufacturing cycle are well-known in the art and not explained in the detail here. With the moulding machine 1 both non-fibre reinforced and fibre reinforced plastic parts can be manufactured.
- the main steps of a simulation identified generally are the following:
- step five when simulating the injection moulding process of a fibre reinforced article are illustrated in the flowchart of FIG. 3 .
- the differential equations for heat flow, fluid flow and stresses and strains are solved using numerical algorithms:
- thermo-physical material temperatures outside the mould i.e. temperature, shrinkage, warpage etc. are calculated using the information obtained from the injection moulding simulation.
- FIG. 4 is a micrograph of a fibre reinforced plastic article, in which the orientation of the fibres after the injection moulding process has finished can be seen.
- the orientation of the fibres in the final product is largely dependent on the flow pattern of the thermoplastic mass during the injection moulding process.
- the fibre orientation is not determined exactly for each single fibre, but rather described by a distribution function.
- a polymer mass includes a large number of short fibres dispersed therein so that the component produced will be made of a short-fibre reinforced thermoplast.
- the mixture of the plastic melt and the dispersed fibres constitutes a complex fluid which is commonly denoted as particle suspension in the terminology of fluid dynamics and physics.
- particle suspension is composed out of two different phases: (i) the solvent, which in our case corresponds to the molten plastic material without the dispersed fibres, and (ii) the particle phase, which consists of all the fibres immersed in the solvent.
- Fibers Spherical particles possessing an axis of rotational symmetry (as shown in FIG. 5 ) are hereinafter denoted as fibres, and the terms particle and fibre are used synonymously except were explicitly indicated otherwise.
- the mass density of the fibre material is comparable to the density of the suspending plastic melt.
- the plastic melt itself has a rather high viscosity at typical temperatures occurring during the mould filling phase.
- the model used to describe the suspension flow of short fibres immersed in a thermoplast melt necessarily has to be a “two phase flow” model that mutually couples the flow of both the particles and the solvent phase and allows for an inhomogeneous particle concentration
- the phenomenon (ii) can be understood as a kind of diffusion process, where the diffusion constant scales like the square of the relative particle size, which is defined as the ratio of the actual size of the suspended particles (i.e. the fibre length, or the radius in the case of spherical particles) to a typical dimension of the flow cavity (e.g. the wall thickness).
- Thermoplast materials display non-Newtonian flow behaviour.
- the rheological properties of the material may be modelled by a scalar viscosity function which depends on temperature as well as on state variables of the flow (generalized Newtonian fluids).
- a scalar viscosity function which depends on temperature as well as on state variables of the flow (generalized Newtonian fluids).
- non-Newtonian flow properties like e.g. shear thinning
- models of this type are used also in the method according to the preferred embodiment of the invention.
- thermoplast matrix material yields mechanical properties which in the solid state are strongly anisotropic and heavily depend on the local distribution of the directions in which the embedded fibres are pointing into.
- anisotropic material behaviour is present also if the material is in a liquid (i.e. molten) state.
- a viscosity tensor To account for this anisotropy one would have to replace the scalar viscosity mentioned above by a viscosity tensor.
- thermoplast melt contains fibres. This is equivalent to the neglect of the influence of the orientation of the dispersed fibres on the rheological properties of the melt.
- the viscosity depends on fibre concentration, but since this is assumed to be constant (see above), this aspect enters only as an a priori known material parameter which contributes to the effective material properties of the thermoplast melt.
- the method according to the preferred embodiment uses a partial decoupling of the calculations of the flow and those of the fibre orientation: while the flow velocity locally influences the orientation of the dispersed fibres, there's negligible influence from the fibre orientation on the flow. Therefore the computation of the flow is carried out independently from the computation of fibre orientation. In this way the local flow velocity of the melt enters the model used for the computation of fibre orientation as a set of external coefficients.
- FIG. 5 illustrates a rigid particle of rotationally elliptic shape whose motion is influenced by the velocity vector field U in the vicinity of the particle.
- the orientation vector p is shown in addition to the quantities (length and diameter d) characterizing the geometry of the particle.
- the direction and size of the flow velocity U is indicated by the direction and length of the corresponding arrows.
- the directions of the velocity vectors are all the same, their length is not, indicating that the flow velocity in the vicinity of the particle is not constant.
- the local amount of change of the flow velocity i.e. the velocity gradient, seems to be the same, as there is a constant increase in the length of the vectors from bottom to top.
- the particle is supposed to move exactly with the local flow velocity (“no slip” boundary condition). If the flow velocity were constant around the particle, this would result in a simple translational motion, i.e. a purely convective transport. Otherwise, in the presence of a velocity gradient, the particle also performs a rotational motion, as indicated by the dashed arrows.
- the most general type of motion performed by the rigid particle is a translation with the “average velocity” around the particle, combined with a rotation around its centre of mass that is driven by the velocity gradient describing the local deviation of the flow velocity from its average value in the vicinity of the particle.
- D Dt ⁇ p ⁇ ⁇ ⁇ t + U ⁇ ⁇ ⁇ ⁇ p on the left hand side (1.h.s.) of eqn. (1) describes pure fibre orientation, FO, transport in the local velocity field U(r,t) of the flow, the right hand side (r.h.s.) models the rotational motion of the particle driven by the effective local velocity gradient tensor ⁇ circumflex over (M) ⁇ .
- FO pure fibre orientation
- G ⁇ 1 2 ⁇ [ ( ⁇ ⁇ U ) + ( ⁇ ⁇ U ) T ] ⁇ ⁇ ( ⁇ ⁇ shear ⁇ ⁇ rate ′′ )
- ⁇ W ⁇ 1 2 ⁇ [ ( ⁇ ⁇ U ) - ( ⁇ ⁇ U ) T ] ⁇ ⁇ ( ⁇ ⁇ vorticity ′′ ) .
- the geometry parameter ⁇ can be regarded as a material parameter.
- D Dt ⁇ p serves as a shorthand for the r.h.s. of Jeffrey's equation (1), and ⁇ p . . . and ⁇ p ⁇ . . . symbolize the gradient and divergence operators defined on the unit sphere S 2 of three dimensional Euclidian space .
- the dimensionless, nonnegative interaction coefficient C I is a material parameter of the suspension. Typically it has a small (positive) value in the range of 10 ⁇ 3 . . . 10 ⁇ 2 for short-fibre reinforced plastics.
- â (2) (r,t) 2nd order FO tensor (or FO matrix) and is, by definition, a real symmetric 3 ⁇ 3 matrix.
- the sign of p 0 drops out of the dyadic product defining this special FO matrix.
- the vector p 0 is an eigenvector of â 0 with eigenvalue 1, and the remaining two eigenvalues are zero with corresponding eigenvectors that lie in the plane orthogonal to p 0 and are arbitrary otherwise.
- This allows for an interpretation of an eigenvalue ⁇ k as the local fraction of fibres oriented along the direction of the corresponding eigenvector E k .
- a real symmetric 3 ⁇ 3 matrix â is a FO matrix if and only if it is positive semidefinite and its trace equals 1.
- the phase space M FT of the FTE is the set of all FO matrices.
- the set M FT is equivalent to the set of all real, symmetric 3 ⁇ 3 matrices that result from moment integrals of the type (3) using properly normalized, but otherwise arbitrary distribution functions.
- a mathematical characterization of the phase space M FT by means of its topological and geometrical properties has been given recently by one of the authors (see [12]). It is of great practical importance to know exactly whether a matrix belongs to the set M FT , as the interpretability of the results of a numerical integration of the FTE requires the dependent variable â (2) to have the special spectral properties as described above during all steps (i.e. also the intermediate ones) of the FO calculation.
- the so called closure problem originates from the fact that at each order of the moment expansion, the DE for the moment â (2n) contains the moment â (2n+2) of the next higher order as a variable. While â (2n) may be expressed in terms of â (2n+2) by means of a simple algebraic identity (i.e. a sum over a pair of two equal indices, see above), the reverse is not possible, so â (2n+2) has to be treated as an unknown. In the FTE this closure problem manifests itself by the appearance of â (4) on the r.h.s. of (5), which prevents the system from being solvable unless it is closed by expressing â (4) as a function of â (2) by means of a closure approximation.
- FTE-hyb the special variant of the FTE (5) combined with the hybrid closure approximation (6).
- FTE-hyb the special variant of the FTE (5) combined with the hybrid closure approximation (6)
- the preferred embodiment of the invention is also based on the FTE-hyb variant of the Folgar-Tucker model.
- the r.h.s. of (5) is formally well defined for arbitrary real symmetric matrices.
- M FT The convexity of M FT allows for the definition of a projection mapping onto M FT which may be combined with any suitable ODE integrator to construct a proper integration method for the FTE (see chapter IV.4 of [9]).
- a real symmetric 3 ⁇ 3 matrix â is a FO matrix if and only if its trace S a equals 1 and its invariants K a and D a are nonnegative.
- FIG. 6 illustrates this statement by a separate analysis of the quadratic and cubic terms and the linear and constant terms of the characteristic polynomial P a ( ⁇ ):
- a positive trace S a obviously provides the existence of positive eigenvalues ⁇ k , while nonnegative values of the two invariants K a and D a prevent the existence of negative ones.
- the conditions S a >0, K a ⁇ 0 and D a ⁇ 0 are not only necessary but also sufficient for all eigenvalues of â to be nonnegative, as the matrix â always has three real eigenvalues.
- the trace condition S a 1 this completes the proof of the above theorem.
- a notion of the geometry of the phase space M FT which is a 5D object according to theorem 1, can be obtained by looking at the diagonal and the off-diagonal elements of FO matrices separately.
- 0 ⁇ x,y,z ⁇ 1, x+y+z 1 ⁇ . (7)
- a formal description of the “off-diagonal” part of the domain M FT may be obtained by introducing the notation (x,y,z) and (u,v,w) for the triples of the diagonal and off-diagonal elements of a real symmetric 3 ⁇ 3 matrix, taking an arbitrary (but fixed) diagonal triple (x,y,z) ⁇ a and formally define the set
- the set N (x,y,z) can be characterized as the set of all off-diagonal triples (u, v, simultaneously satisfying the following pair of inequalities, as explained with respect to Theorem 2 above: K a ⁇ 0 u 2 +v 2 +w 2 ⁇ xy+xy+zx, (9) D a ⁇ 0 u 2 x+v 2 y+w 2 z ⁇ 2 uvw ⁇ xyz. (10)
- the (formal) fibration M FT ⁇ (x,y,z) ⁇ a (x,y,z) ⁇ N (x,y,z) obtained by introducing the sets ⁇ a and N (x,y,z) helps to get a picture of the overall structure of M FT (see FIG. 10 ):
- the individual “fibres” may be visualized by a procedure that locally attaches the set N (x,y,z) of admissible off-diagonal triples to its “base point” (x,y,z) ⁇ a , and the subsequent variation of this base point throughout the whole triangle set ⁇ a covers the whole phase space.
- phase space M FT is a complex mathematical object.
- the confinement of any solution trajectory t â (2) (t) of the FTE, which is naturally defined as an evolution equation in the real vector space of symmetric 3 ⁇ 3 matrices, to the phase space domain necessarily implies the fulfillment of the invariant inequalities (9) and (10) combined with the unit trace condition. This fact inevitably turns the FTE into a DAS.
- section 7.7 a procedure is presented that provides a suitable kind of invariant control. This procedure has been implemented in a preferred embodiment.
- the exact FO matrix â (2) is by definition symmetric and satisfies the trace condition.
- the interaction coefficient C I is a small positive number (typically 0 ⁇ C I ⁇ 10 ⁇ 2 , see also sec. 1.2), it can be seen that ⁇ a will become negative if evaluated with an FO matrix which has a dominant eigenvalue ⁇ j ⁇ 1 with corresponding eigenvector E k pointing along the eigendirection of the largest negative eigenvalue of the shear rate tensor, as in this case it may be estimated
- the choice of a suitable method for the numerical integration of the FTE depends on the mathematical classification of the equation type as well as aspects related to the specific algebraic form of the FTE.
- the general structure of the closed FTE shows that it constitutes a coupled system of hyperbolic partial differential equations (PDEs) of convection-reaction type for the elements a ij (2) of the FO matrix as dependent variables, as explained in detail in the following paragraph.
- PDEs hyperbolic partial differential equations
- the l.h.s. consists of a simple first order partial differential operator of transport or convection type with the local flow velocity U(r,t) governing the decoupled, purely convective transport of the elements a ij (2) of the FO matrix that are the dependent variables of the eqn. (16).
- the algebraic structure of the various terms on the r.h.s. of (16) shows that the r.h.s.—just like the FO matrix itself, and as required by mathematical consistency—constitutes a symmetric tensor function of 2 nd order, which is denoted as ⁇ circumflex over (F) ⁇ (2) ( . . . ) in the following abstract (but equivalent) form of eqn. (16):
- the second one constitutes a system of ordinary differential equations (ODEs) which is in general coupled and nonlinear.
- ODEs ordinary differential equations
- the flow solver i.e. the software that models the flow of the suspension, yields the state variables of the fluid, among them the flow velocity U(r,t) and its gradient tensor ⁇ U(r,t), by a solution of the discretized transport equations for mass, momentum and energy, at discrete instants of time t n in all computational cells located around discrete points r m in space which are contained in the filled part ⁇ (n) of the overall computational domain covering the mould cavity, the gating system and the inlet.
- the flow computations imply a computation of the domain ⁇ (n+1) at time t n+1 depending on its previous state ⁇ (n) and the new velocity field U (n+1) This can be done by using a volume of fluid (VOF) method.
- VIF volume of fluid
- Calculating the new flow front and the new domain ⁇ (n+1) yields new values of all state variables in the cells of ⁇ (n+1) at time t n+1 .
- the new values y m (n+1) y(r m ,t n+1 ) at time t n+1 in all computational cells located around the points r m of the newly filled domain ⁇ (n+1) shall be computed by a numerical solution of the PDE
- ⁇ ⁇ t ⁇ y F ⁇ ( y ) with step size ⁇ t n+1 , using the velocity gradient ⁇ U(r m ,t n+1 ) provided by the flow solver in the domain ⁇ (n+1) .
- FIG. 11 illustrates this operator splitting variant.
- ⁇ ⁇ t ⁇ y F ⁇ ( y ) with half step size ⁇ t n+1 /2, using the velocity gradient ⁇ U(r m ,t n+1 ) provided by the flow solver in the domain ⁇ (n+1) .
- ⁇ ⁇ t ⁇ y F ⁇ ( y ) with half step size ⁇ t n+1 /2, using the velocity gradient ⁇ U(r m ,t n+1 ) provided by the flow solver in the domain ⁇ (n+1) .
- a numerical method is used to extend the known values of the FO matrix within the computational cells of the “old” domain ⁇ (n) into the cells of the new domain ⁇ (n+1) .
- the computation of the “new” domain ⁇ (n+1) is performed by a modified VOF method as one part of the algorithm applied in the method according to the preferred embodiment for the numerical solution of the flow equations (i.e. the conservation equations for mass, momentum and energy).
- the values of the FO matrix are left unchanged during the extension step in those cells that are common to both domains.
- the domain ⁇ (n+1) contains a number of “newly filled cells” where an initial assignment of reasonable values for the elements of the FO matrix is needed. In accordance with the preferred embodiment this is achieved by means of a weighted average corresponding to the mass transport within a computational cell from/into its neighbouring cells according to the previously computed mass flow.
- the particle concentration is assumed to be homogeneous and the FO matrix results from a volume averaging procedure on a macroscopic level, it is assumed that a cell will get a FO contribution from its neighbouring cells proportional to the net amount of fluid mass transported into it.
- the initialization procedure is compatible with the (theoretically required) topological structure of the phase space of the FT model, which is an important property of this procedure.
- frountain flow characterizes the overall macroscopic flow pattern near the free surface at the front in the case of a large class of viscous, Non-Newtonian fluids.
- particles upstream near the flow front are transferred from the core region to the wall boundaries.
- This effect actually happens “automatically” because of the material properties of the fluid and does not require any additional modelling, i.e.: “fountain flow” is an emergent phenomenon, at least in 3D flow computations based on the Navier-Stokes equations with appropriate Non-Newtonian constitutive laws.
- this is not the case if the flow calculations are based upon simplified models (e.g.
- the FTE model is a system of hyperbolic transport equations coupled by their r.h.s. (i.e. a system of convection-reaction type with nonlinear reaction term, see above). Therefore it is not appropriate—i.e.
- the hyperbolic structure of the (closed) FTE requires the initialization of the FO matrix in the computational cells in (as well as near) the inlet at every time step of the mould filling simulation as a boundary condition. Therefore an appropriate choice of this initial FO state has to be made.
- an isotropic FO state â (2) 1 ⁇ 3 ⁇ circumflex over (1) ⁇ (corresponding to a random FO distribution) is chosen for this purpose as explained below.
- the FO state is strongly influenced by a high shear rate, as it is quickly driven to its “final” state of local quasi-equilibrium. Therefore the FO state observed at the ingates—this is where the melt actually enters the part—is completely determined by its flow history throughout the runner system and largely independent of its initial state assumed at the inlet.
- an analysis of the analytical structure of the FTE as well as its kinematics shows that the assumption of a random orientation at the inlet is the optimal choice in view of a subsequent adaption by the flow field in the runner system near the inlet, because a random orientation state yields full coupling of all components of the velocity gradient.
- Step 1 set initial conditions and boundary conditions on the newly filled cells
- Step 2 move fibre orientation according to flow field
- Step 3 calculate fibre rotation according to velocity gradient.
- Hybrid closure approximations as defined by eqns. (6) and (6a/b) experience stability problems especially in cases where the velocity gradient had a complicated structure—i.e. is not of simple shearing/stretching type but reflects a complex 3D flow pattern—and the size of the time step (as determined by the flow solver) becomes rather large.
- the deviation of the scalar orientation factor f s (â (2) ) to negative values is a primary source of these instabilities: once this factor becomes negative, the numerical solution quickly becomes unstable and diverges exponentially to values far away from the phase space set admissible for FO matrices.
- the definition (19) is denoted as stabilized hybrid closure approximation. Numerical experiments have shown that the confinement of the values of ⁇ tilde over (f) ⁇ s (â (2) ) to the interval [0,1] prevents the development of severe instabilities in the considered test examples.
- the stabilized hybrid closure has been successfully tested in a variety of 3D injection moulding simulation.
- the 2 nd order FO tensor â (2) which is the dependent variable of the closed FTE as presented in eqn. (16), is a symmetric 3 ⁇ 3 matrix.
- a ij (2) a ji (2) a priori constitute a set of six mutually independent variables
- the FTE is a coupled system of six PDEs.
- the algebraic structure of the FTE formally admits arbitrary symmetric 3 ⁇ 3 matrices, the matrices have to fulfil a number of additional conditions formulated as restrictions on their invariants that qualifies them as FO matrices.
- both the trace condition and the PDE for the diagonal element a 33 (2) are fulfilled identically (i.e. as formal algebraic identities), and it suffices to consider only the remaining set of five components of the FO matrix and the coupled system of their PDEs further on.
- the method according to the preferred embodiment deviating from the “standard approach” of eliminating one of the diagonal elements via the unit trace condition—uses all six elements of the FO matrix and equations of the FTE system for FO computation.
- the control approach is used especially to keep the trace of the numerically computed FO matrix approximately at its required unit value.
- a reasonable control term should be compatible with the scaling behaviour of the r.h.s. function of the FTE w.r.t. a rescaling of the velocity gradient (see section 7.4 on flow controlled time integration for further details on this point), and it should contain a tuning parameter that allows for an adjustment of a “soft” or “hard” control, the latter effectively resembling to a projection in the limit of “infinitely hard” control.
- the parameter a is required to be positive, but not necessarily constant in time.
- the 3 ⁇ 3 matrix ⁇ circumflex over (b) ⁇ is required to be symmetric with unit trace, but otherwise arbitrary.
- the matrix ⁇ circumflex over (b) ⁇ defines the “direction” of the control term (20). It may be either a constant or variable in time. The latter includes the possibility to define ⁇ circumflex over (b) ⁇ as a function of â (2) .
- Different choices of the matrix ⁇ circumflex over (b) ⁇ correspond to different variants of the control term.
- D Dt ⁇ a ⁇ ( 2 ) F ⁇ hyp ( 2 ) ( ⁇ ... ⁇ ) + C ⁇ hyb ⁇ ( ⁇ , a ⁇ ( 2 ) , ⁇ ⁇ U ) ( 21 ) of the closed FTE with stabilized hybrid closure must also be considered.
- the control term enters on the r.h.s. of the ODE (18b), which thereby assumes the form of eqn. (21) with the material derivative D/Dt replaced by the partial derivative ⁇ / ⁇ t.
- Tr( ⁇ hyb ( . . . )) ( ⁇ circumflex over ( ⁇ ) ⁇ a ) ⁇ [1 ⁇ Tr(â (2) )]
- the specific form of the control term is tailored to modify (15a/b) according to
- the trace of any numerical solution of (21) is kept close to the required value 1 by the control term (20), as this term forces all solutions having Tr(â (2) )>1 in the direction of ⁇ circumflex over (b) ⁇ towards lower trace values, and those solutions having Tr(â (2) ) ⁇ 1 are correspondingly forced towards larger trace values (also in the direction of ⁇ circumflex over (b) ⁇ ).
- large values of ⁇ may cause problems when used with explicit ODE integration methods, as in this case the large trace corrections push the numerical solution to either side of the hyperplane in an alternating way and thereby induce spurious oscillations. It has been shown [18] that a choice of ⁇ within a relatively wide range of intermediate values leads to proper numerical results without undesired artefacts induced by the control term.
- Numerical schemes for the integration of ODE systems account for the “strength” of the r.h.s. function by a proper (preferably adaptive) choice of the step size. In this way it is attempted to avoid inaccuracies occurring due to a coarse stepping across intervals of large values or a strong change of the r.h.s. function, as well as taking too small steps across the regions where the (absolute) values of the r.h.s. function are rather small.
- a proper choice of the step size as well as the integration scheme one is able to control the numerical error of ODE integration up to a desired limit.
- the general task is a numerical integration of the coupled system (18c) of ODEs in the time interval [t n , t n+1 ] with a global numerical error ⁇ FO that is uniform over all cells of the domain of filled cells.
- This can be achieved by exploiting the special property (24) of the r.h.s. function ⁇ circumflex over (F) ⁇ (2) ( . . . ) for a scaling of the velocity gradient, the r.h.s. function and the ODE system (18c) in the following way:
- ⁇ U also the parameter ⁇ max depends on the spatial vector r m that labels the local computational cell as well as on the time coordinate t n or t n+1 at which the velocity gradient enters the r.h.s. function.
- the integration scheme used in the method according to the preferred embodiment uses a set of simple integration rules belonging to class of one step methods (see sections 16.1 of [38] and 7.2.1-7.2.3 of [39]) included herein by reference.
- the specific integration rules used within the FO module of the method according to the preferred embodiment are:
- the proposed method chooses specifically the integration rule which achieves the required error bound with the minimum number of r.h.s. function evaluations as estimated according to the relations presented in the points a) to d) above.
- the size of the time step ⁇ t n+1 as determined by the flow is typically rather small ( ⁇ t n+1 ⁇ 10 ⁇ 2 . . . 10 ⁇ 4 s) compared to the total mould filling time (which is of the order of seconds)
- the dimensionless quantity ⁇ n+ (m) can be of order O(1), as the values of ⁇ max may become rather larger (of order 10 . . . 100 s ⁇ 1 ) because of the small gap size and the large viscosity of the polymer melt.
- ⁇ FO ⁇ 1 in fact typically ⁇ FO 1 holds
- the size of the error bounds grows monotonically with increasing value of the order parameter p (we always have 0 ⁇ p ⁇ p+1 ⁇ 1), so the error bounds relevant to the formulation of the algorithm given below are always ordered according to 0 ⁇ FO ⁇ 1 ⁇ 2 ⁇ 4 ⁇ 1.
- a minimum threshold of e.g. ⁇ min 10 ⁇ 6 is a reasonable choice for typical mould filling applications.
- the algorithm described above is used in a preferred embodiment. It defines a “hybrid” integration rule for the “Rotation Step” ODE system (18b) in all cells of the domain ⁇ n+1 over the time interval [t n ,t n+1 ] with a uniform global error smaller than ⁇ FO and a minimum number of evaluations of the r.h.s. function of (18b).
- the application of the integration rules to the scaled version (25) of (18b) is done “in place” by using the scaled velocity gradient in the evaluation of the r.h.s. function and the computation of the step size h based on the size of the scaled interval length ⁇ n+1 (m) .
- ⁇ ⁇ ⁇ ⁇ a ⁇ ( 2 ) F ⁇ ( 2 ) ⁇ ( a ⁇ ( 2 ) , ⁇ ⁇ U _ ) + C ⁇ hyb ⁇ ( ⁇ 0 , a ⁇ ( 2 ) , ⁇ ⁇ U _ ) ( 29 ) has to be considered in place of (25) as a basis for the discrete time steps of the integration algorithm.
- the time integration scheme implemented in the FO module of the method according to the preferred embodiment performs the numerical integration of the “Rotation Step” ODE system by application of the “hybrid” integration algorithm as defined in this section to the ODE system (29) including dynamical trace stabilization by means of the control term (20).
- FCTI flow controlled time integration
- the most important factor which directly affects the computational cost of FO computation is the choice of the closure approximation.
- the stabilized hybrid closure yields reasonable accuracy at low computational cost and is used by the method.
- the additional operations to compute ⁇ circumflex over (N) ⁇ a by eqn. (31a) are (i) 1 multiplication to get 1 ⁇ 2 ⁇ a and (ii) 3 “adds” to subtract 1 ⁇ 2 ⁇ a from the diagonal elements of the matrix ⁇ circumflex over (N) ⁇ .
- the number of operations saved amounts to a multiplication of all components of the FO matrix by the prefactor ⁇ a and the subtraction operations for ⁇ a â (2) . Therefore the total number of operations is smaller if eqns. (30a) & (31a) are used for the evaluation of the r.h.s. function instead of (30) & (31).
- the restricted scalar orientation factor ⁇ tilde over (f) ⁇ s is computed according to (19). Substituting ⁇ tilde over (f) ⁇ s for f s in (32) then results in “stabilized prefactors” ⁇ tilde over ( ⁇ ) ⁇ a , ⁇ tilde over ( ⁇ ) ⁇ 1 and ⁇ tilde over ( ⁇ ) ⁇ g without affecting the computational costs.
- ⁇ 1 1 ⁇ 3( ⁇ tilde over ( ⁇ ) ⁇ a ) ⁇ [1 ⁇ Tr ( â (2) )] (33) is added to the prefactor ⁇ tilde over ( ⁇ ) ⁇ 1 which leads to a modified r.h.s.
- ⁇ a ( ⁇ tilde over ( ⁇ ) ⁇ a ) ⁇ [1 ⁇ Tr(â (2) )]/Tr(â (2) ) that has to be added to the prefactor ⁇ tilde over ( ⁇ ) ⁇ a .
- the FO-Matrix, the matrix ⁇ M and the matrix ⁇ circumflex over (F) ⁇ storing the result of the evaluation of the r.h.s. function ⁇ circumflex over (F) ⁇ (2) (â (2) , ⁇ U) are assigned to corresponding vector quantities.
- mapping â â ⁇ circumflex over (M) ⁇ + ⁇ circumflex over (M) ⁇ T ⁇ â defines a linear mapping in the six-dimensional vector space of real symmetric 3 ⁇ 3 matrices, which can be formally written as a matrix-vector product ⁇ circumflex over (M) ⁇ a in R 6 described by the real 6 ⁇ 6 matrix ⁇ circumflex over (M) ⁇ , whose elements are either zero or given by simple algebraic terms of the elements of ⁇ circumflex over (M) ⁇ .
- the CN scheme yields the identification
- M ⁇ ( 2 ⁇ M 11 0 0 0 2 ⁇ M 31 2 ⁇ M 21 0 2 ⁇ M 22 0 2 ⁇ M 32 0 2 ⁇ M 12 0 0 2 ⁇ M 33 2 ⁇ M 23 2 ⁇ M 13 0 0 M 23 M 32 M 22 + M 33 M 12 M 13 M 13 0 M 31 M 21 M 11 + M 33 M 23 M 12 M 21 0 M 31 M 32 M 11 + M 22 ) . ( 35 ⁇ a )
- This operation can also be written as a matrix-vector product ⁇ G M , where the matrix elements of ⁇ are related to the elements of ⁇ via
- a _ ⁇ ⁇ ⁇ v ⁇ A ⁇ ⁇ ⁇ v , v ⁇ ⁇ 1 , 2 , 3 ⁇ 2 ⁇ A ⁇ ⁇ ⁇ v , v ⁇ ⁇ 4 , 5 , 6 ⁇ ⁇ ⁇ for ⁇ ⁇ ⁇ ⁇ ⁇ 1 , ... ⁇ , 6 ⁇ . ( 35 ⁇ b )
- the final row of the table shows that a single evaluation of the r.h.s. function is obtained at the computational cost of 96 -operations, 84 ⁇ -operations and 3 function calls to compute the square root of a (double precision) floating point number as well as the minimum and maximum of a pair of such numbers.
- the computational cost of addition and multiplication operations is about the same, a call to a min- or max-function costs about 1.5-2 operations, and the cost of a square root computation amounts approximately to 6-10 operations (i.e. on average 8 operations, depending on the required accuracy).
- DTS dynamical trace stabilization
- any numerical solution of the FTE having nonnegative eigenvalues ⁇ k (or equivalently: nonnegative 2 nd and 3 rd invariants K a and D a ) and S a ⁇ 1 can be interpreted as an FO matrix in practice.
- An alternative procedure consists of a combination of an “uncontrolled” (or partially controlled) integration procedure with a projection operation that maps the numerical solution back to its admissible domain.
- Such a “passive” procedure results in a valid integration scheme that preserves the accuracy of the “uncontrolled” scheme if the operations of numerical integration and subsequent projection are applied in every time step (see ch. IV.4 of [9] on projection methods for a detailed discussion).
- phase space M FT is a convex set ( ⁇ Theorem 1 in section 3.), for each real, symmetric 3 ⁇ 3 matrix there exists a unique matrix in M FT at “minimum distance” (measured in a suitable metric, see below). This defines the projection mapping required for the third step of the above procedure. Further details of phase space projection are discussed below.
- a monitoring of the invariants by checking the inequalities K a ⁇ 0 and D a ⁇ 0 can be done at the cost of additional 22 operations per time step for each cell.
- a check of the invariants K a and D a is the most efficient way to determine whether a real, symmetric 3 ⁇ 3 matrix belongs to the set M FT of FO matrices, as a check of the conditions ⁇ k ⁇ 0 on the eigenvalues requires an explicit computation of the latter.
- P a characteristic polynomial
- a numerical diagonalization of the matrix is the most expensive method to compute the eigenvalues. Therefore such a procedure is not recommended unless the eigenvectors are also of interest (e.g. as a part of the phase space projection procedure discussed below).
- the result of the process which is a distribution function that describes the likeliness of the orientation of the fibres in a given area of the article is presented in graphical or numerical form on a display of a computer workstation (not shown).
- This could be the display of the computer or workstation on which the calculations are performed, or this could be on a display of a computer that is networked to the computer on which the simulation is performed.
- a mould or product designer will use the results of the simulation to improve and the quality of the article that results from the injection moulding process.
- the results of the simulation may also be used by engineers to reduce the cost for manufacturing the article concerned.
- the advantage of a reliable information about the fibre information allows engineers to have a better understanding and information before determining the strength, rigidity and stability characteristics of the article, since the orientation of the fibres, which fibres typically have much higher strength characteristics than the polymer material, have a decisive influence on the strength, rigidity and stability characteristics of the article. Further, the fibre orientation has an influence on warping effects that may occur when injection moulding a polymer masses with fibres suspended therein. By knowing the fibre orientation, the warping and other stress creating the commission to effect can be better predicted or to design changes be avoided.
- results of the simulation can also be transmitted to other applications such as CAD software.
- results of the simulation can be used in interactive process between the design software and the simulation software.
- the invention has numerous advantages. Different embodiments or implementations may yield one or more of the following advantages. It should be noted that this is not an exhaustive list and there may be other advantages which are not described herein.
- One advantage of the invention is that the distribution of the fibre orientation fibre reinforced articles of manufacture can be determined at a significantly reduced computational effort.
- Advantage of the present invention is that the distribution of the fibre orientation in fibre reinforced articles of manufacture can be determined with an increased accuracy.
- Another advantage of the present invention is that the distribution of the fibre orientation in fibre reinforced articles of manufacture can be determined faster.
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Abstract
Description
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step 1, providing a digital representation of the geometry of the simulation domain; -
step 2, enmeshment, which is subdivision of the calculation domain into many small elements, which are the bases for discretizing the differential equations (utilizing different solution algorithms) and in this way finding the solutions to the physical phenomena to be simulated; -
step 3, attaching the necessary physical data for the different materials domains into the simulation model (data base or data bank); -
step 4, specifying the boundary conditions for the simulation project, -
step 5, simulate injection moulding process (this step will be a claimed in greater detail below); and -
step 6, displaying the results as a graphical or numerical presentation on the display of a computer such as a workstation.
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step 1 the initial conditions for the thermophysical material properties and the flow front are set; -
step 2 the thermal equations for the whole domain and flow equations on all fluid cells are solved using the conservation of mass, energy and momentum equations; -
step 3, in this step the flow front is moved and the boundary conditions are adopted according to new flow front; - in
step 4 the fibre orientation and transport is calculated from the flow velocity obtained in the previous steps. This step will be explained in greater detail below. Initial conditions are applied to the newly filled cells. Only cells containing fluid material are considered; - in
step 5 additional quantities like chemical reactions are calculated, and it is verified if cells solidify; - in
step 6 it is verified if the in mould injection moulding process is finished; if not the simulation continues with the next time step and the process returns to step 2; - in
step 7 the properties of the article after ejection from mould are calculated.
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which is written here in compact Eulerian form. While the convective (or material) derivative
on the left hand side (1.h.s.) of eqn. (1) describes pure fibre orientation, FO, transport in the local velocity field U(r,t) of the flow, the right hand side (r.h.s.) models the rotational motion of the particle driven by the effective local velocity gradient tensor {circumflex over (M)}. In the ideal special case of infinitely slender fibres (i.e. aspect ratio ra→∞) the tensor {circumflex over (M)} is identical to the velocity gradient tensor ∇U, in the general case of fibres having finite aspect ratio (0<ra<∞) it is defined by the term
containing the fibre geometry parameter λ=ra 2−1)/(ra 2+1). This parameter encodes how particle geometry affects the rotational motion of the fibres in the case of rotationally symmetric ellipsoidal particles.
The shear rate and vorticity tensors are related to the effective velocity gradient tensor via the identities
{circumflex over (M)}=Ŵ+λĜ Ĝ=½λ({circumflex over (M)}+{circumflex over (M)} T)Ŵ=½({circumflex over (M)}−{circumflex over (M)} T) (1c).
Inserting these identities into (1) and taking into account that pT·Ŵ·p=0 yields Jeffery's equation in the alternative form
Yet another form of Jeffery's equation may be obtained by rewriting the first term on the r.h.s. of (1d) using the identity −Ŵ·p=ŴT·p=½rot U×p, which relates the vorticity tensor to the rotation rot U of the flow velocity vector field (see e.g. [3]).
with the FO distribution function Ψ as dependent variable. Here
serves as a shorthand for the r.h.s. of Jeffrey's equation (1), and ∇p . . . and ∇p● . . . symbolize the gradient and divergence operators defined on the unit sphere S2 of three dimensional Euclidian space . According to the approach of Folgar and Tucker [4], the introduction of a diffusion coefficient Dr=CIγeff proportional to the effective shear rate γeff=√{square root over (2GijGij)} of the local velocity gradient yields a simple model of fibre-fibre interaction in concentrated suspensions. Here the Gij are the components of the shear rate tensor Ĝ as defined in (1b), and the term under the square root—using the Einstein summation convention—is a short hand for its self-contraction GijGij=Σi,jGij 2=Ĝ:Ĝ. The dimensionless, nonnegative interaction coefficient CI is a material parameter of the suspension. Typically it has a small (positive) value in the range of 10−3 . . . 10−2 for short-fibre reinforced plastics. We note that in incompressible (as well as nearly incompressible) flows, the relative weakness of the “stochastic” diffusion term—compared to the term representing the “deterministic” Jeffery dynamics—can be the source of stability problems.
2.3 Fibre Orientation Tensors and the Folgar-Tucker Equation
â (2)(r,t)= S
(in index notation: aij (2)(r,t)= S
â (4)(r,t)= S
(in index notation: aij kl (4)(r,t)= S
The hierarchy of moment equations mentioned above is obtained for the moments of each order by interchanging the derivative and integration operations, i.e.
replace
by the terms on the r.h.s. of the Fokker-Planck equation (2) and evaluate the corresponding integrals analytically. If this procedure is applied to the FO matrix â(2), the so called Folgar-Tucker equation (FTE) is obtained as the first nontrivial in the hierarchically organized series of moment equations:
As in Jeffery's equation, the convective derivative on the l.h.s. of (5) describes the pure transport of the local FO state (represented by the FO matrix â(2) in this order of the moment expansion) due to the translational motion of the fibres in an Eulerian reference frame, while the first two terms on the r.h.s. of (5) model their rotational motion driven by the local effective velocity gradient {circumflex over (M)}. The 3rd term on the r.h.s. of (5) results from the presence of the diffusion term in the Fokker-Planck eqn. (2). At the level of the FTE it yields a damping effect that drags the FO matrix towards the isotropic state â(2)=⅓{circumflex over (1)}.
In its Eulerian form (5) the FTE is a coupled system of 1st order PDEs of convection-reaction type. From the Lagrangean viewpoint (5) is a coupled system of ODEs for the components of â(2).
2.4 Basic Properties of the FO Matrix
 hyb (4) [â (2) ]:=f s(â (2))·Â qu (4) [â (2)]+(1−f s(â (2)))·Â lin (4) [â (2)] (6)
which, despite some well known drawbacks, is an accepted choice because of its algebraic simplicity and numerical robustness [7]. The closure Âhyb (4) is defined as a (convex) interpolation between two closures of simpler type: the quadratic closure defined as
 qu (4) [â (2) ]:=â (2) â (2)(i.e.( qu (4) [â (2)])ijkl :=a ij (2) a kl (2) in index notation) (6a)
which yields exact results in the special case of an uniaxial orientation distribution, and the linear closure given by
which is exact in the isotropic case. The interpolation weight between these extreme cases is provided by the scalar orientation factor
f s(â (2)):=1−27det(â (2)). (6c)
As the determinant det(â(2)) is an invariant of the FO matrix, the same is true for the scalar orientation factor.
P a(μ)=det(μ{circumflex over (1)}−â)=μ2(μ−S a)+K a μ−D a
of a real symmetric 3×3 matrix.
and Da=det(â) are invariants of the matrix. (In the literature these invariants occasionally are denoted by I1=Sa, I2=Ka and I3=Da.) The algebraic characterization of FO matrices may be formulated in terms of these invariants according to
Δa:={(x,y,z)∈|0≦x,y,z≦1,x+y+z=1}. (7)
This provides a necessary condition which characterizes FO matrices w.r.t. their diagonal elements and yields an invariant representation of the “diagonal part” of the phase space set MFT.
of all “admissible” off-diagonal triples belonging to a fixed diagonal triple. Algebraically the set N(x,y,z) can be characterized as the set of all off-diagonal triples (u, v, simultaneously satisfying the following pair of inequalities, as explained with respect to
K a≧0 u 2 +v 2 +w 2 ≦xy+xy+zx, (9)
D a≧0 u 2 x+v 2 y+w 2 z−2uvw≦xyz. (10)
A ij kl (4) =A j ikl (4) , A ij kl (4) =A ij lk (4) , A ij kl (4) =A (4) klij (11)
i.e. the 4th order tensor Â(4) is required to be symmetric w.r.t. the first and second index pairs (ij) and (kl) as well as the interchange (ij)(kl) of both pairs. If it is assumed that â(2) is a solution of (5) augmented by a closure approximation â(4)←Â(4)[â(2)] with orthotropic symmetry properties (11), we may formally derive the following differential equation (abbrev.: DE) for its trace (see [17]):
and the DE (12) for the trace simplifies to
with a prefactor
φa=6D r+2λf s(Ĝ:â (2))+2λ/7(1−f s)Tr(Ĝ). (15b)
-
- (i) In the special case of an incompressible flow field (i.e. Tr(Ĝ)=div U=0) the prefactor assumes the simplified form φa=6Dr+fs2λ(Ĝ:â(2)).
- (ii) In the case of slender fibres it may always be assumed λ=1, and if the local orientation state described by â(2) is approximately uniaxial (i.e. one of its eigenvalues μk is close to 1), the value of the scalar orientation factor fs=1−27 det(â(2)) also is approximately 1 as the determinant of â(2) is close to zero. In this way the simplified expression φa≈6Dr+2(Ĝ:â(2)) is obtained, which approximates the exact value of φa under the specified assumptions.
- (iii) By substitution of Dr=CIγef f and insertion of the spectral representation â(2)=ΣkμkEk Ek into the contraction Ĝ:â(2)=ΣijGijaij (2) a modified form of the approximate expression for the prefactor is obtained:
-
- (iv) In the last step the components of shear rate tensor Ĝ to the effective shear rate γef f=√{square root over (2GijGij)} are normalized. The normalized shear rate tensor Ĝ{circumflex over (′)}:=γef f −1Ĝ has the same eigenvectors as Ĝ, zero trace and therefore—just the same as Ĝ—negative eigenvalues. As the components of Ĝ{circumflex over (′)} are of
order 1 by construction, the tensor Ĝ{circumflex over (′)} necessarily has at least one negative eigenvalue with an absolute value oforder 1.
- (iv) In the last step the components of shear rate tensor Ĝ to the effective shear rate γef f=√{square root over (2GijGij)} are normalized. The normalized shear rate tensor Ĝ{circumflex over (′)}:=γef f −1Ĝ has the same eigenvectors as Ĝ, zero trace and therefore—just the same as Ĝ—negative eigenvalues. As the components of Ĝ{circumflex over (′)} are of
and therefore get φa≈6γef f[CI±2]<0.
on the l.h.s. and the mathematical notation â(4)←Â(4)[â(2)] symbolizing a closure approximation on the r.h.s. of (5), which yields an equivalent formulation of the closed FTE:
of this equation, using a condensed notation that hides all parameter dependencies and does not discriminate between explicit and implicit dependencies of the component functions Fij (2)( . . . ) on the FO matrix or the velocity gradient. Reverting from index notation to the full tensor notation used in eqns. (17a/b), the simplified version
of these equations is obtained.
6. Numerical Integration of the FTE: “Operator Splitting”
of convection-reaction type. One approach that has proven to be robust and flexible especially in the case of nonlinear r.h.s. functions F( . . . ) starts from an equivalent reformulation of the PDE as
and proceeds by a separate treatment of the two terms on the r.h.s. given by the linear differential operator −U·∇ . . . and the “operator” determined by the function F( . . . ). In the mathematical literature this approach is known as [23-37] “method of fractional steps”, “splitting method” or simply “operator splitting” (see [28-31] for alternative approaches). The numerical integration of an equation having the form
by “operator splitting” makes use of the numerical (or in some cases even analytical) solutions of the two separate equations
and
obtained from the full equation by setting either of the two operators on the r.h.s. to zero. The first equation is equivalent to the homogeneous convection eqn.
the second one constitutes a system of ordinary differential equations (ODEs) which is in general coupled and nonlinear. This type of approach is used in the preferred embodiment. Using the notation of the eqns. (17a/b), the application of the splitting approach to the closed FTE leads to the partial equations
which are treated as separate subproblems within the framework of the “operator splitting” method. The physical effect modelled by eqn. (18a) is the spatial redistribution of the FO statistics (as encoded by the elements of the FO matrix) within the filled domain of the mould cavity due to a purely convective transport of the fluid mass according to the flow velocity, while eqn. (18b) completely neglects the effects of convective transport and solely accounts for the local rate of change of the FO distribution due to the rotational kinematics of the fibres driven by the local velocity gradient as well as the mutual interaction among the fibres. Hereinbelow several variants are described that show how the (numerical) solutions of both subproblems may be combined to yield an approximate solution of the full equation (16) (or its equivalent (17a/b) in abstract notation).
6.1 “Simple Operator Splitting”
starting from the values ym (n)=y(rm,tn) defined in the “old” domain Ω(n) which are already known from the previous computation step.
-
- 1. Extension step: Starting from ym (n)=y(rm,tn) in the cells of the domain Ω(n), compute an initialization
y m (n) in all cells of the new domain Ω(n+1). - 2. Convection step: Starting from the initial values
y m (n) provided by the extension step, compute intermediate values {tilde over (y)}m (n+1) by a numerical solution of the convection equation
- 1. Extension step: Starting from ym (n)=y(rm,tn) in the cells of the domain Ω(n), compute an initialization
with step size Δtn+1, using the flow velocity U(rm, tn+1) computed by the flow solver in the domain Ω(n+1).
-
- 3. Rotation step: Starting from the initial values {tilde over (y)}m (n+1) provided by the preceding convection step, compute the final values ym (n+1)=y(rm, tn+1) by a numerical solution the ODE system
with step size Δtn+1, using the velocity gradient ∇U(rm,tn+1) provided by the flow solver in the domain Ω(n+1).
with a time discretization error of 1st order—i.e. O(Δtn+1)—in the step size and is used in the method according to the preferred embodiment. Details on the three steps of this procedure will be explained in subsequent sections.
-
- (i) starts by a rotation step on Ω(n) using the “old” velocity gradient ∇U at time tn, then
- (ii) proceeds with an “intermediate” step to extend the results of (i) from Ω(n) to Ω(n+1) and
- (iii) finishes with a convection step using the flow velocity U at time tn+1.
-
- (i) starting with an extension step of the known values ym (n) from Ω(n) to Ω(n+1) as described above, then
- (ii) performing a rotation step followed by
- (iii) a convection step
using the “new” values of U and ∇U provided by the flow solver at time tn+1 in Ω(n+1) for both steps (ii) and (iii).
6.2 “Symmetric Operator Splitting”
-
- 1. Extension step: Starting from ym (n)=y(rm,tn) in the cells of the domain Ω(n), compute an initialization
y m (n) in all cells of the new domain Ω(n+1). - 2. Pre-Rotation step: Starting from the extension
y m (n) of the known values to Ω(n+1) provided by the extension step, compute the pre-rotated valuesy m (pre) by a numerical solution of the ODE system
- 1. Extension step: Starting from ym (n)=y(rm,tn) in the cells of the domain Ω(n), compute an initialization
with half step size Δtn+1/2, using the velocity gradient ∇U(rm,tn+1) provided by the flow solver in the domain Ω(n+1).
-
- 3. Convection step: Starting from
y m (pre) as initial values provided by the pre-rotation step, compute intermediate values {tilde over (y)}m (n+1) by a numerical solution of the convection equation
- 3. Convection step: Starting from
with full step size Δtn+1, using the flow velocity U(rm,tn+1) computed by the flow solver in the domain Ω(n+1).
-
- 4. Post-Rotation step: Starting from the initial values {tilde over (y)}m (n+1) provided by the preceeding convection step, compute the final values ym (n+1)=y(rm,tn+1) by a numerical solution of the ODE system
with half step size Δtn+1/2, using the velocity gradient ∇U(rm,tn+1) provided by the flow solver in the domain Ω(n+1).
which has a time discretization error of 2nd order—i.e. O(Δtn+1 2)—in the step size.
-
- (i) with an extension of the known values ym (n) to the new domain Ω(n+1),
- (ii) proceeds with a “pre-convection” step of half step size in the new domain using the flow velocity U(rm,tn+1), then
- (iii) performs a full rotation step on Ω(n+1) using the velocity gradient ∇U(rm,tn+1) and
- (iv) finishes with another half step size “post-convection” step using the flow velocity U(rm,tn+1),
which finally results in an approximation of ym (n+1)=y(rm,tn+1) that is also of 2nd order accuracy. As in the case of “simple splitting” there is yet a third variant that interchanges the initial extension step and the pre-rotation step, starting with the latter and thereby using the “old” values of the velocity gradient ∇U(rm,tn) on Ω(n).
determined by the partial functions Fk( . . . ). Possibly some of the partial functions involve linear operators, i.e. Fk (y)={circumflex over (L)}k·y. In this case one might consider some (or all) of these linear terms on the r.h.s. of the partial convection equation, i.e.
which thereby remains linear, and leave some (or all) of the genuinely nonlinear functions Fj( . . . ) for treatment within a single ODE
or a list
of separate ODEs as explained above.
-
- The formulation the FTE using the complete set of 6 independent elements of the FO matrix (opposed to the “standard procedure” of using the trace condition to eliminate one of the diagonal elements and reduce the number of dependent variables of the FTE by one);
- The addition of a “penalty” control term to the r.h.s. of the FTE that transforms the hyperplane defined by the trace condition into a stable integral manifold of the FTE;
- The exploitation of the specific scaling behaviour of the r.h.s. function of the FTE w.r.t. the components of the velocity gradient to construct an integration method which selects the time integration scheme according to the size of the local shear rate (max. component of the velocity gradient).
- The implementation of a “stabilized hybrid closure” that contains a scalar orientation factor that is confined to the interval [0,1].
- The implementation of an efficient procedure for the evaluation of the special r.h.s. function of the FTE with hybrid closure with a minimum number of operations.
 hyb (4) [â (2) ]:={tilde over (f)} s(â (2))·Â qu (4) [â (2)]+(1−{tilde over (f)} s(â (2)))·Â lin (4) [â (2)]
{circumflex over (f)} s(â (2):=min(1,max(1−27det(â (2)), 0))∈[0,1]. (19)
-
- The control term has to vanish identically if the trace condition is already fulfilled.
- If the numerical solution fails to fulfil the trace condition, the control term must drive the numerical solution back to the Tr(â)=1 hyperplane.
D/Dt Tr(â (2))=Tr(D/Dtâ (2))=Tr({circumflex over (F)} (2)( . . . ))= . . .
Ĉ hyb(α,â (2),∇ U)=(α−{tilde over (φ)}a)·[1−Tr(â (2))]·{circumflex over (b)},α>0,Tr({circumflex over (b)})=1.
of the closed FTE with stabilized hybrid closure must also be considered. Likewise the control term enters on the r.h.s. of the ODE (18b), which thereby assumes the form of eqn. (21) with the material derivative D/Dt replaced by the partial derivative ∂/∂t. As the trace of the control term (20) evaluates to Tr(Ĉhyb( . . . ))=(α−{circumflex over (φ)}a)·[1−Tr(â(2))], the specific form of the control term is tailored to modify (15a/b) according to
of the control term identically leads to the trace DE (22) and thus to a stabilization of the Tr(â(2))=1 hyperplane as described above for the special case of the (stabilized) hybrid closure. If we allow the symmetric,
7.4 Flow Controlled Time Integration
-
- the “integration rule” (Euler, midpoint or 4th order Runge Kutta) and
- the (dimensionless) local step size as well as
- the local number of steps of this size with the chosen rule
adapted to the “strength” of the local r.h.s. function as determined by the values of the local velocity gradient. The scheme is different from known approaches of “adaptive step size control” for numerical ODE integration, as it exploits the scaling behaviour of the r.h.s. function of eqns. (16) or (18b) w.r.t. the components of the velocity gradient and is specifically adapted to the FTE system. The procedure of choice for the integration rule and the number and size of the local time steps inherent to the scheme is a heuristic approach that is based on the theoretical discretization error of the used integration rules. Both aspects of the scheme are explained in detail below.
{circumflex over (F)} (2)( . . . )=â (2) ·{circumflex over (M)}+{circumflex over (M)} T ·â (2)−({circumflex over (M)}+{circumflex over (M)} T):Â (4) [â (2)]+2D r[{circumflex over (1)}−3â (2)].
In order to resolve all dependencies on the velocity gradient ∇U explicitly one has to substitute the definitions (1a/b) of the effective velocity gradient and the shear rate tensor, i.e.
as well as the identity {circumflex over (M)}+{circumflex over (M)}T=2λĜ and the formulas Dr=CIγef f, γef f=v√{square root over (2Ĝ:Ĝ)} defining the rotational diffusion parameter and the effective shear rate. For the following considerations it will be helpful to suppress the indirect dependencies of the function {circumflex over (F)}(2)( . . . ) on the FO matrix via the closure function Â(4)[â(2)] and on the velocity gradient via the effective shear rate as well as the dependence on the constant model parameters CI and λ and thus to rewrite the algebraic expression of the r.h.s. function (as already done for the r.h.s. of eqn. (17c)) in a simplified form as
{circumflex over (F)} (2)(â (2) ,∇ U)=â (2) ·{circumflex over (M)}+{circumflex over (M)} T ·â (2)−2λĜ:Â (4) [â (2)]2C Iγeff[{circumflex over (1)}−3â (2)], (23)
leaving only the dependence on the FO matrix â(2) and the velocity gradient ∇U in the argument list of {circumflex over (F)}(2)( . . . ). An equivalent reformulation of the ODE system (18b) (corresponding to (17c)) using the r.h.s. function (23) can be written in the form
{circumflex over (F)} (2)(â (2) ,σ∇ U)=σ{circumflex over (F)} (2))(â (2) ,∇ U), (24)
expressing the scaling behaviour of the function {circumflex over (F)}(2)( . . . ) w.r.t. its 2nd argument.
-
- Determine the value of the component of the velocity gradient with the largest absolute value, i.e.:
(Note that with ∇U also the parameter γmax depends on the spatial vector rm that labels the local computational cell as well as on the time coordinate tn or tn+1 at which the velocity gradient enters the r.h.s. function.)
-
- Introduce the scaled velocity gradient
∇ Ū:=γmax −1 ∇U and the scaled time coordinate τ:=γmaxt—note that both are dimensionless quantities, and this scaling is applied only locally in the cell rm, and in the time interval [tn, tn+1]—and transform the ODE (18c) to the scaled form:
- Introduce the scaled velocity gradient
-
- using the scaled quantities and eqn. (24).
Δτn+1 (m):=γmax(r m ,t n+1)·Δt n+1, (26)
but with r.h.s. functions that, as the scaled velocity gradient
-
- i. The scaled velocity
∇ Ū gradient is by construction a dimensionless quantity, with the absolute values of its components equal or smaller than 1. - ii. The values of the FO matrix elements as well as those of the 4th order tensor elements supplied by the closure function Â(4)[â(2)] are also limited by 1.
- iii. Therefore all components of the r.h.s. function {circumflex over (F)}(2)( . . . ) are of order O(1) when evaluated with
∇ Ū, while the largest components of {circumflex over (F)}(2)( . . . ) have absolute values comparable with γmax when evaluated with ∇U instead.
- i. The scaled velocity
∥{circumflex over (F)}(2)({circumflex over (a)}(2),¤ U)∥=O(γmax),∥{circumflex over (F)}(2)({circumflex over (a)}(2)
-
- i. an “integration rule” with sufficiently small discretization error as well as
- ii. a suitable number of substeps to cover the scaled time interval.
-
- the simple forward Euler rule, which is a method of 1st order accuracy and requires 1 evaluation of the r.h.s. function per step,
- the “midpoint” or 2nd order Runge-Kutta (RK2) rule, which is a method of 2nd order accuracy and requires 2 evaluations of the r.h.s. function per step, and
- the 4th order Runge-Kutta (RK4) rule, which is a method of 4th order accuracy and requires 4 evaluations of the r.h.s. function per step.
-
- a) A method of order p requires p evaluations of the r.h.s. function per substep.
- b) If an ODE (system) is integrated numerically over an interval of total size Δτ with N equidistant substeps of size h=Δτ/N, the total error ∈tot accumulated at the final substep of the interval may be estimated as: ∈tot˜Δτ·hp.
- c) If this total error is required to be smaller than a preselected threshold value ∈max, the size of the substeps is bounded by h<(∈max/Δτ)1/p. Likewise the number of substeps has to be larger than N>Δτ·(Δτ/∈max)1/p.
- d) The integration over the total interval with a total error smaller than ∈max may be performed taking N substeps with an order p method provided the interval size is bounded by Δτ<(∈max·Np)1/(p+1). This implies that a single substep (i.e. N=1) of size h=Δτ is sufficient if Δτ<∈max 1/(p+1) holds.
-
- (i) either a single step with one of the three integration rules or
- (ii) multiple substeps of appropriate size using the RK4 rule,
where the choice depends on the relative size of Δτn+1 (m) compared to the required error threshold ∈FO (see below). As this error bound is the same for all computational cells of the domain Ω(n+1), the integration is performed with a uniform error ∈FO independent of the local values of Δτn+1 (m) (or likewise γmax(rm,tn+1)=Δτn+1 (m)/Δtn+1).
-
- 1. First evaluate γmax:=∥∇U∥∞ and compute the scaled velocity gradient
∇ Ū:=γmax −1 ∇U and the scaled interval size Δτn+1 (m):=γmax(rm,tn+1)·Δtn+1. - 2. Check if Δτn+1 (m)≦∈min step 12.1.
- a. If yes, then skip the ODE integration (i.e. do nothing), keep the previous value of the FO matrix in the cell as the new (updated) value and exit the procedure.
- b. If not, then go to step 12.2.
- 3. Check if ∈min<Δτn+1 (m)≦∈1.
- a. If yes, then update the previous value of the FO matrix in the cell by a single Euler step of size h=Δτn+1 (m) using
∇ Ū for the evaluation of the r.h.s. function and exit the procedure. - b. If not, then go to step 12.3.
- a. If yes, then update the previous value of the FO matrix in the cell by a single Euler step of size h=Δτn+1 (m) using
- 4. Check if ∈1<Δτn+1 (m)≦∈2.
- a. If yes, then update the previous value of the FO matrix in the cell by a single “midpoint” (RK2) step of size h=Δτn+1 (m) using
∇ Ū and exit the procedure. - b. If not, then go to step 12.4.
- a. If yes, then update the previous value of the FO matrix in the cell by a single “midpoint” (RK2) step of size h=Δτn+1 (m) using
- 5. Check if ∈2<Δτn+1 (m)≦∈4.
- a. If yes, then update the previous value of the FO matrix in the cell by a single “4th order Runge-Kutta” (RK4) step of size h=Δτn+1 (m) using
∇ Ū and exit the procedure. - b. If not, then go to step 12.5.
- a. If yes, then update the previous value of the FO matrix in the cell by a single “4th order Runge-Kutta” (RK4) step of size h=Δτn+1 (m) using
- 6. In the general case ∈4<Δτn+1 (m) the update of the FO matrix is computed by performing several RK4 steps with an appropriate step size.
- a. The minimum number of steps to achieve the required ∈FO accuracy is the smallest integer N that satisfies the inequality N>Δτ·(Δτ/∈FO)1/p. Using the functions int( . . . ), returning the integer part of a floating point number, and max( . . . , . . . ), returning the larger of two numbers, the integer N≧1 may be computed by the formula:
N=max(int(Δτ·(Δτ/∈FO)1/p)+1,1). - b. The required step size is then computed by h=Δτn+1 (m)/N.
- c. Once N and h are computed, update the previous value of the FO matrix in the cell by N steps of the RK4 rule with step size h (using
∇ Ū on the r.h.s.) and exit the procedure.
- a. The minimum number of steps to achieve the required ∈FO accuracy is the smallest integer N that satisfies the inequality N>Δτ·(Δτ/∈FO)1/p. Using the functions int( . . . ), returning the integer part of a floating point number, and max( . . . , . . . ), returning the larger of two numbers, the integer N≧1 may be computed by the formula:
- 1. First evaluate γmax:=∥∇U∥∞ and compute the scaled velocity gradient
Tr({circumflex over (F)} cl (2)(â (2) ,∇ U))=Tr(γmax {circumflex over (F)} cl (2)(â (2),γmax −1∇ U))=γmax Tr({circumflex over (F)} cl (2),
and, using the control factor α=α0·γmax, obtain the equivalent expression
for the control term (20a). The expression on the r.h.s. now contains γmax as a separate factor and a term depending on {circumflex over (F)}cl (2)( . . . ) that is evaluated with the scaled velocity gradient
Ĉ cl(α,â (2) ,∇ U)=γmax ·Ĉ cl(α0 ,â (2) ,∇ U),
which also shows that the control term in its general form (20a) has exactly the same scaling behaviour as the “uncontrolled” r.h.s. function {circumflex over (F)}cl (2)( . . . ) w.r.t. a scaling of the velocity gradient by γmax if the control parameter is chosen as α=α0·γmax.
Ĉ hyb(α,â (2) ,∇ U)=γmax·(α0−
where the “rescaled” prefactor
has to be considered in place of (25) as a basis for the discrete time steps of the integration algorithm.
{circumflex over (F)}(â (2),∇ U)=â (2) ·{circumflex over (N)}+N T ·â (2)−φa â (2)+φ1{circumflex over (1)}+φg Ĝ M (30)
{circumflex over (N)}:={circumflex over (M)}− 2/7(1−f s)Ĝ M , Ĝ M :={circumflex over (M)}+{circumflex over (M)} T=2λĜ (31)
in place of the effective velocity gradient matrix {circumflex over (M)} given by 1(a). The remaining three terms on the r.h.s. all have the form φX{circumflex over (X)} of a product of a scalar prefactor φX that multiplies a matrix quantity {circumflex over (X)}. The prefactors are given by the set of formulas
Ĝ M=2λĜ and Tr(Ĝ M)=2λTr(Ĝ), where Tr(Ĝ)=div U.
{circumflex over (N)} a :={circumflex over (N)}− 1/2φ a{circumflex over (1)}={circumflex over (M)}− 2/7(1−f s)Ĝ M½φa{circumflex over (1)} (31a)
and use the matrix {circumflex over (N)}a instead of {circumflex over (N)} for the evaluation of the r.h.s. function. Making use of the algebraic identity
â (2) ·{circumflex over (N)} a +{circumflex over (N)} a T ·â (2) =â (2) ·{circumflex over (N)}+{circumflex over (N)} T ·â (2)−φa â (2)
the explicit computation of the term φaâ(2) is omitted, and the r.h.s. function is redefined according to
{circumflex over (F)} (2)(â (2),∇ U)=â (2) ·{circumflex over (N)} a +{circumflex over (N)} a T ·â (2)+φ1{circumflex over (1)}+φg Ĝ M. (30a)
Ĉ hyb(α,â (2),∇ U)=(α−{tilde over (φ)}a)·[1−Tr(â (2))]·{circumflex over (b)},α>0,Tr({circumflex over (b)})=1
leads to further operations necessary for the evaluation of the r.h.s. The general structure of this control term is given by Ĉhyb( . . . )={tilde over (φ)}b{circumflex over (b)} with a prefactor {tilde over (φ)}b=(α−{tilde over (φ)}a)·[1−Tr(â(2))] and therefore is of the same form φX{circumflex over (X)} as discussed above. The prefactor {tilde over (φ)}b is absorbed into the one of the prefactors {tilde over (φ)}1 or {tilde over (φ)}a if either {circumflex over (b)}=⅓{circumflex over (1)} or {circumflex over (b)}=â(2)/Tr(â(2)) are chosen for the projection matrix. In the first case the term
φ1=⅓(α−{tilde over (φ)}a)·[1−Tr(â (2))] (33)
is added to the prefactor {tilde over (φ)}1 which leads to a modified r.h.s. function
{circumflex over (F)} (2)(â (2) ,∇ U)=â (2) ·{circumflex over (N)} a +{circumflex over (N)} a T ·â (2)+({tilde over (φ)}1+φ1){circumflex over (1)}+φg G M. (30b)
-
- 1. Input: (â(2),∇U) & Parameters: λ, CI, α
- Auxiliary variables: {circumflex over (F)}, {circumflex over (N)}a, ĜM, λ+, λ−, fs, {tilde over (f)}s, {tilde over (φ)}a, {tilde over (φ)}1, {tilde over (φ)}g, φ1, ζ, ξ1, . . . , ξ6
- 2. Initialize {circumflex over (N)}a with the effective velocity gradient matrix computed by (1a):
{circumflex over (N)} a←λ+(∇ U)+λ−(∇ U)T ={circumflex over (M)}, λ ±:=½(λ±1) - 3. Compute the symmetric matrix ĜM←{circumflex over (N)}a+{circumflex over (N)}a T and its trace ξ1←Tr(ĜM).
- 4. Compute ξ2=2Dr, from the contraction ζ←ĜM:ĜM by ξ2←(CI/λ)√{square root over (2ζ)}.
- 5. Compute the scalar orientation factor fs←1−27 det(â(2)), its bracketed version {tilde over (f)}s←min (1, max (fs,0))∈[0,1] and the term ξ3←(1−{circumflex over (f)}s)/7.
- 6. Compute the contraction ξ4←ĜM:â(2).
- 7. Compute the prefactors according to (32) using the values stored in the auxiliary variables ξk by the following formulas:
{tilde over (φ)}a←3ξ2 +{tilde over (f)} sξ4−ξ3ξ1,{tilde over (φ)}1←ξ2+ξ3(⅕ξ1−ξ4),{tilde over (φ)}g←⅖ξ3 - 8. Compute the term φ1←⅓(α−{tilde over (φ)}a)·[1−Tr(â(2))], then compute {tilde over (φ)}1←{tilde over (φ)}1+φ1.
- 9. Compute the matrix {circumflex over (N)}a using the aux. variables ξ5←2ξ3 and ξ6←½{tilde over (φ)}a. The computation is supposed to be done by the following sequence of operations:
{circumflex over (N)} a ←{circumflex over (N)} a−ξ5 Ĝ M {circumflex over (N)} a ←{circumflex over (N)} a−ξ6{circumflex over (1)}. - 10. Initialize the r.h.s. result matrix by computing {circumflex over (F)}←â(2)·{circumflex over (N)}a+{circumflex over (N)}a T·â(2). a Then successively complete the evaluation of the r.h.s. function (30b):
{circumflex over (F)}←{circumflex over (F)}+{tilde over (φ)} 11 {circumflex over (F)}←{circumflex over (F)}+φ g Ĝ M - 11. Result: {circumflex over (F)}(2)(â(2),∇U)←{circumflex over (F)}
Reformulation of the FTE in Vector Form Using “Contracted Notation” (CN)
- 1. Input: (â(2),∇U) & Parameters: λ, CI, α
|
1 | 2 | 3 | 4 | 5 | 6 | ||
(ij) = | (11) | (22) | (33) | (23) = (32) | (13) = (31) | (12) = (21) |
(ji) | ||||||
A 44 =A 23 , A 55 =A 13 , A 66 =A 12 , A 25 =A 46 , A 14 =A 56 , A 45 =A 36,
that reduce the number of independent elements of  to 15. The normalization conditions aij (2)=Σk=1 3Aij kk (4)=Σk=1 3Aikj k (4) and the trace condition Σk−1 3akk (2)=1 yield a set of algebraic relations that reduces the number of independent matrix elements to an even smaller value (see [22] for details).
(Â (4) :Ĝ M)ij=Σk,l=1 3 A ij kl (4)(G M)kl=Σν=1 3 A μν(G M)ν2·Σν=4 6 A μν(G M)84
using the index assignments μ(ij),ν(kl) as given by the CN scheme. This operation can also be written as a matrix-vector product Ā·GM, where the matrix elements of Ā are related to the elements of  via
so the term Ā[a] represents the closure approximation in CN.
Computational Cost of the Proposed Algorithm
Step | Quantity | # | # ⊕ | |
2 | λ±, {circumflex over (N)}a ← {circumflex over (M)} | 17 | 8 | — |
3 | ĜM, Tr(ĜM) | — | 8 | — |
4 | ζ ← ĜM:ĜM, ξ2 | 10 | 5 | {square root over ( . . . )} |
5 | det(â(2)), fs, {tilde over (f)}s, ξ3 | 13 | 7 | min( . . . ) |
max( . . . ) | ||||
6 | ξ4 ← ĜM: |
7 | 5 | — |
7 | {tilde over (φ)}a, {tilde over (φ)}1, {tilde over (φ)}g | 6 | 4 | — |
8 | φ1, {tilde over (φ)}1 ← {tilde over (φ)}1 |
2 | 5 | — |
9 | ξ5, ξ6, {circumflex over (N)}a ← {circumflex over (N)}a - . . . | 8 | 12 | — |
10 | {circumflex over (F)} ← â(2) · {circumflex over (N)}a + {circumflex over (N)}a T · |
33 | 30 | — |
{circumflex over (F)} ← {circumflex over (F)} + . . . | ||||
Σ | {circumflex over (F)}(2) (â(2), ∇ U)← {circumflex over (F)} | 96 | 84 | 3 |
-
- As the matrix {circumflex over (N)}a is not symmetric, it is stored as a 3×3 matrix. An extra storage of {circumflex over (M)} is not necessary if {circumflex over (N)}Q is initialized with the computation of {circumflex over (M)}.
- The symmetric matrix ĜM is needed in matrix form for the computation of {circumflex over (N)}a (→step 9.), but also appears as a 6-vector in the final step 10.
- Storage and assignment operations are not counted, as they their contribution to the overall computational costs is negligible.
- The number of auxiliary variables is reduced by reusing already existing variables once their value is no longer needed. This has not been done in the version of the algorithm proposed above, since this would reduce the clarity of presentation of the algorithm.
- The contraction operation of a pair of symmetric matrices (as occurring in steps 4. and 6.) is implemented with 7- and 5⊕-operations using CN. (In matrix notation it is defined by in {circumflex over (m)}:{circumflex over (n)}=Tr({circumflex over (m)}T·{circumflex over (n)})=Σi,j=1 3mijnij.)
- The determinant of a real symmetric 3×3 matrix (→step 5.) is computed with 11 {circle around (x)}- and 5 ⊕-operations using CN.
- The assembly of the matrix {circumflex over (N)}a performed in step 9. requires 6 {circle around (x)}- and 12 ⊕-operations if an auxiliary variable storing ĜM as a symmetric 3×3 matrix is used, plus 2 multiplications to compute the variables ξ5 and ξ6.
- The matrix operation {circumflex over (F)}←â(2)·{circumflex over (N)}a+{circumflex over (N)}a T·â(2) requires 27 {circle around (x)}- and 21 ⊕-operations using CN.
- Any operation of the type . . . +β{circumflex over (1)} that adds (or subtracts) a multiple of the unit matrix requires only three additions of β to the diagonal elements.
-
- The “standard” procedure would start with the computation of the matrix {circumflex over (M)}, the 6-vector
and the scalar parameter 2Dr (see steps 2. to 4.), which in sum requires 46 operations plus a square root computation.
-
- The operation ââ·{circumflex over (M)}+{circumflex over (M)}T·â corresponding to {circumflex over (M)}·a requires 48 operations if the matrix-vector product is carried out analytically in advance and only the resulting formulas for the six components are evaluated numerically.
- The computation of the matrix-vector product Ā·GM and its subtraction from the r.h.s. requires 66+6=72 operations.
- The addition of 2Dr·1 and the subtraction of 6Dr·a (using 6Dr=3/2·2Dr) require another 3+12+1=16 operations.
-
- The computation of the restricted scalar orientation factor {tilde over (f)}s and the auxiliary variable ζ2 are done by
step 5. of the effective algorithm and requires 23 operations (counting 3 operations for the nested min(0, max( . . . , 1)) calls). The auxiliary variable ζ1=ζ2/5 is computed by one additional division, so the amount of operations required to compute {tilde over (f)}s and ζ1/2 is 24. - The matrix  is initialized by Aμν←{tilde over (f)}saμaν, which takes 2 multiplications for each of the 21 independent matrix elements of the upper triangle, or 42 operations in sum. (The remaining matrix elements are assigned by symmetry.)
- The matrix elements of ζ1{circumflex over (D)} are computed by a single operation (i.e. the computation of 3ζ1) and a number of assignments of either ζ1 or 3ζ1 to the corresponding nonzero matrix elements. Likewise the entire update operation Â←Â−ζ1{circumflex over (D)} requires only the subtraction of either ζ1 or 3ζ1 from the corresponding entries of Â. As it is only necessary to perform these subtractions on the upper triangular elements of Â, the total operation count for the update operation reduces to 10 (i.e. 9 subtractions plus 1 operation to compute 3ζ1).
- The matrix Ê contains 12 different expressions, of which only 9 have to be computed by a single addition or multiplication. (The rest is obtained by assignments.) As none of the 12 expressions can a priori be assumed to be zero, the computation of ζ2Ê needs 12 multiplications, so the total amount of operations to compute ζ2Ê is 21 for the independent elements of this matrix. The remaining matrix elements are subsequently obtained by assignment.
- The final step in the assembly procedure for  consists of the update operation Â←Â+ζ2Ê, which requires 21 operations that add the upper triangles of the matrices  and ζ2Ê and the assignments to obtain the remaining matrix elements of the lower triangle.
- The computation of the restricted scalar orientation factor {tilde over (f)}s and the auxiliary variable ζ2 are done by
and Da=det(â) of the matrix.
â|→â′=1/S a â(i.e.:a′ ij =a ij /S a) Tr(â′)=1 (37)
and has several favourable properties:
-
- If λk are the eigenvalues of the matrix â, the eigenvalues of the rescaled matrix â′ are given by μ′k=μk/Sa, so
- (i) they do not change their sign if Sa>0, and
- (ii) their numerical values are only slightly rescaled if Sa≈1
- (as guaranteed by DTS).
- The corresponding eigenvectors are not affected by the rescaling operation.
- If λk are the eigenvalues of the matrix â, the eigenvalues of the rescaled matrix â′ are given by μ′k=μk/Sa, so
commutes with the trace operation, it is possible to derive an evolution equation for the trace in a straightforward manner (→
-
- 1. an integration step using the methods described in
sections - 2. an invariant monitoring step to determine if the matrix computed in the preceding integration step is still an FO matrix, and
- 3. a phase space projection step which maps the matrix back to the phase space set MFT if the result of the monitoring step has been negative (i.e. the invariant conditions have been violated).
- 1. an integration step using the methods described in
which altogether can be evaluated with 11 additions and 13 multiplications. As the trace Sa is computed in every time step during the numerical integration of the FTE, a monitoring of the invariants by checking the inequalities Ka≧0 and Da≧0 can be done at the cost of additional 22 operations per time step for each cell.
which is itself induced by the scalar product {circumflex over (m)}|{circumflex over (n)}=Tr({circumflex over (m)}T·{circumflex over (n)}) in the vector space of real 3×3 matrices. The restriction of these quantities to the six-dimensional subspace of symmetric matrices is straightforward. It can be shown [18] that for any real 3×3 matrix {circumflex over (m)} there exists a unique matrix â*∈MFT such that the distance dF({circumflex over (m)},â) between {circumflex over (m)} and the elements â of MFT is minimized precisely by â=â*.
-
- The eigenvectors of â* are the same as those of the matrix {circumflex over (m)}.
- The triple of eigenvalues (μ*1, μ*2, μ*3) of â* is the unique point of the triangle set (see eqn. (7) in
section 3 andFIG. 7 )
Δa:={(x,y,z)∈|0≦x,y,z≦1,x+y+z=1} - that has the smallest Euclidian distance in R3 to the point (μ1, μ2, μ3) given by the triple of eigenvalues of the matrix {circumflex over (m)}.
and the algorithm to actually compute the value of the projection mapping consists of the following steps:
-
- 1. Given a real symmetric 3×3 matrix â∈Rs 6 as input, compute its invariants Sa, Ka and Da.
- 2. Check the conditions Sa=1, Ka≧0 and Da≧0. If all conditions are fulfilled, then â∈MFT already, and the projection mapping is just the identity:
â∈M FT {circumflex over (P)} FT [â]=â. (39a) - In this case assign the input matrix â to output and exit. Otherwise (i.e. if either Ka<0 or Da<0) execute the following steps:
- 3. Compute the eigenvalues μk and corresponding eigenvectors Ek of the matrix (i.e. â·Ek=μkEk). This step may be formally represented as:
-
- 4. Next find the unique point μ*=(μ*1, μ*2, μ*3)∈Δa having minimal Euclidian distance to μ=(μ1, μ2, μ3) in R3, i.e.:
-
- 5. Finally compose the value â*={circumflex over (P)}FT[â] of the projection mapping by
{circumflex over (P)} FT [â]=â*=Σ k=1 3μ*k E k E k a* ij=Σk=1 3μ*k(E k)i(E k)j. (39d)
- 5. Finally compose the value â*={circumflex over (P)}FT[â] of the projection mapping by
-
- In
Step 1. the invariants Ka and Da of the input matrix are computed by (38). - In
Step 2. only the conditions Ka≧0 and Da≧0 are checked, and the input matrix is left unchanged and assigned to output if both conditions are fulfilled. - The results of
Step 3. are obtained by numerical matrix diagonalization, e.g. by iterative cyclic Jacobi rotations (see [38], ch. 11.1 or [39], ch. 6.5.2) or a single Givens/Householder reduction step and subsequent QR iterations (see [42] or [38], ch. 11.2). - Actually
Step 4. is carried out only if at least one of the input eigenvalues μk is negative, so the solution point μ*=(μ1*, μ*2, μ*3)∈Δa is always located on the edges (including the cornerpoints) of the triangle set Δa. - Using the “trace rescaled” eigenvalues ũk=μk/Sa (see eqn. (37) and the subsequent remarks on this subject) confines the minimization problem that has to be solved to determine μ* according to (39c) to the plane Sa=1 fixed by the three cornerpoints (1,0,0), (0,1,0) and (0,0,1) of the triangle Δa. This “plane” minimization problem can be solved equivalently in R2, e.g. in the (μ1, μ2)—plane, by finding the unique pair (μ*1, μ*2) located on the edges of the projected triangle
{tilde over (Δ)}a:={(μ1,μ2)∈|0≦μ1,μ2≦1,μ1+μ2≦1} - (i.e. the orthogonal projection of Δa to the (μ1,μ2)—plane) that has the smallest Euclidian distance to the pair ({tilde over (μ)}1,{tilde over (μ)}2). The third coordinate of μ* is then given by
μ*3=1−(μ*1+μ*2). - Since Sa≈1 by DTS, the algorithm that solves the “plane” minimization problem yields a very good approximation to the exact solution of (39c), while it is much simpler and can be implemented more efficiently than an algorithm that computes μ* directly from (39c) in R3.
- In
Step 5. the formula to compute the individual elements of the matrix â* is given by a*ij=Σk=1 3μ*kRikRjk in terms of the matrix elements Rij of the rotation matrix {circumflex over (R)}=(E1,E2,E3) that has been computed previously inStep 3.
8. Implementation
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